 |
TEDD
TEDD is an acronym for Thermal
Equalization and Distribution Device. It
is designed to reduce the wide
temperature variation across the diameter
of the melt stream as it exits the
extruder. The temperature can have a
variety of profiles depending on machine
speed and screw design.
Peak to peak variations
as much as 30o F are common
and this translates into large viscosity
variations. Cut and try modifications
must be made to the die to produce the
product profile required. This means the
die will produce the right profile over a
rather limited production rate range.
|
The TEDDÒ
takes advantage of the fact that the
temperature profile exiting the die is
symmetrical about the axis of the
machine. It turns the melt flow inside
out several times just before the melt
arrives at the die. This periodically
moves hot material to a relatively cold
zone and vice versa. Temperature
variations are substantially reduced,
melt viscosity is now constant, and the
die will perform consistently over a wide
production rate range.
VISCOSITY
AND PRESSURE DROP CONSIDERATIONS
| Most
polymeric materials are shear
sensitive. That is to say, their
viscosity is dependent on the
shear rate to which they are
exposed. Usually an increased
shear rate produces a lowering of
viscosity and is referred to as
shear thinning. Viscosity versus
shear rate data is usually
provided by the polymer
manufacturer in the form of a
graph on log/log paper. We list
below the shear rate and pressure
drop formula for each of the
devices we have described and
others together with the units
involved. Main pipe inside
diameter = D inches
Main product flow rate = Q gpm
Shear rate = g
sec-1
Viscosity = m cP
Pressure drop = dP psi
Axial length = L inches
Additive fraction = F
Number of mixing elements = n
|

|
| Device |
A/t
Value |
Shear
rate |
Pressure
drop |
Comments |
| Open
pipe |
---------- |
39.2Q/D3 |
22.73x10-6Qm L/D4 |
Hagen-Poiseuille
Equation |
| Helix |
np |
96.0Q/D3 |
205x10-6Qm n/D3 |
Helix
L/D ratio = 1.5:1 |
| L/H
unit |
8/p2
F |
215Q/D3 |
5.9x10-4Qm /D3 |
Each
hole dia. = 0.45D |
| H/L
unit |
3.6/F |
81.7Q/Dt2 |
22.1Qm L/Dt3 |
Where
annulus dia.= 2D/3 |
|
KOMAX
SYSTEMS, INC. INTRODUCES
A NEW STATIC MIXER SYSTEM
FOR HIGH
VISCOSITY PRODUCTS
(U.S. Patent 5,484,203)
- A Single Injection Point
allows pressurized clearing action from the additive pump if
needed. The built in check valve prevents back flow of
polymer into the additive supply.
- The TADD
Injector distributes
additive across the inlet of the ULTRA
mixer. It is less than one pipe diameter in length and has
a low pressure drop.
- The ULTRA
Mixer generates multiple
interstices with a uniform spatial distribution to give
100% utilization of the mixer volume and superior additive
dispersion with low pressure drop

| Device |
A/t
Value |
Shear
rate |
Pressure
drop |
Comments |
| SIDD |
288/p2 F |
593Q/D3 |
12.6x10-4
Qm
/D3 |
Each
hole dia. = 0.3D |
| PARAFLO |
8pN/F |
Contact factory for
shear rate and pressure drop
calculations. |
| HOME | THE COMPANY | OUR CLIENTS | PRODUCT
SPECS | CAD LIBRARY | CONTACT US |
| DETAILED
SPECIFICATIONS | CAD DRAWING |

|